JP5526502B2 - Exhaust gas purification catalyst and method for producing the same - Google Patents

Description

  The present invention relates to an exhaust gas purifying catalyst suitable for a process for purifying exhaust gas discharged from an internal combustion engine, and a method for manufacturing the same.

In recent years, in order to remove harmful substances such as hydrocarbon compounds (HC), carbon monoxide (CO), and nitrogen oxides (NO _x ) contained in exhaust gas discharged from an internal combustion engine, alumina (Al ₂ Exhaust gas purifying catalysts in which noble metal particles such as platinum (Pt) are supported on a metal oxide carrier such as O ₃ ) are widely used. In conventional exhaust gas purification catalysts, a large amount of noble metal particles is used in order to improve the durability of the noble metal particles against ambient fluctuations. However, using a large amount of noble metal particles is not desirable from the viewpoint of protecting earth resources.

  In order to reduce the amount of noble metal used, the particle diameter of the noble metal particles supported on the carrier may be reduced. The smaller the particle size of the noble metal particles, the larger the specific surface area. Therefore, the amount of noble metal used for obtaining the desired catalyst purification performance can be reduced. However, if the particle diameter of the noble metal particles is small, they may be thermally agglomerated (sintered) with each other due to high temperatures or long-term use, which may reduce durability.

Therefore, the noble metal particles are supported on the first compound, the first compound supporting the noble metal particles is encapsulated in the second compound, and the first compounds supporting the noble metal are supported by the second compound. An exhaust gas purification catalyst having a separated structure has been developed (Patent Document 1). In the exhaust gas purifying catalyst having such a structure, the noble metal particles are supported on the first compound, and the noble metal particles are physically fixed to the first compound. The first compounds supported by the noble metal particles are separated from each other by the second compound, so that the first compounds supporting the noble metal are prevented from contacting and aggregating with each other. By these things, durability can be improved by preventing the noble metal particles from aggregating after durability.
International Publication No. 2007/052627 Pamphlet

In the exhaust gas purifying catalyst described in Patent Document 1, the first compound supporting noble metal particles is made of an oxide containing Ce as a main component. For this reason, this conventional exhaust gas purifying catalyst has an air-fuel ratio (air-fuel ratio) under a condition where a rich-lean atmosphere fluctuation periodically occurs centering on the stoichiometric air-fuel ratio (stoichiometry). In the case of exhaust gas purification, it is possible to mitigate the fluctuation of the atmosphere in the vicinity of the catalyst particles due to the oxygen absorption / release capability of the oxide containing Ce as a main component, thereby enabling the sintering of precious metals. Suppression of oxygen and supply of active oxygen necessary for the three-way reaction are appropriately performed, and high purification performance is achieved. Is not shed without increasing the production cost and environmental load, it is possible to maintain the effect of enhancing the activity of the noble metal particles by the first compound.

  However, when the above-mentioned exhaust gas purification catalyst is applied to a gasoline direct injection engine or a diesel engine that is operated on the lean side of the stoichiometric ratio of the air-fuel ratio, noble metal oxidation occurs and the exhaust gas Purification performance may be reduced.

In order to solve the above problems, the exhaust gas purifying catalyst according to the present invention, a noble metal, a first compound, made from a second compound, the noble metal is supported on the first compounds, the noble metal the first compound supported is encapsulated in the second compound, the first compound in which the noble metal is supported with each other includes a unit structure separated by the second compound, and,
The noble metal consists Pt, wherein said first compound is mainly composed of Ti, and _consists TiO _2, TiO 2 -ZrO ₂ complex compound or _TiO 2 -CeO ₂ composite compound, the second compound is [ The main point is that the main component is one or more selected from Al and Si.

  The method for producing an exhaust gas purifying catalyst according to the present invention is a method for producing the above exhaust gas purifying catalyst, wherein the first compound in contact with the noble metal is converted into a colloid having a primary particle diameter of 100 nm or less. And a step of forming a second compound around the first compound in contact with the colloidal noble metal.

  The method for producing an exhaust gas purifying catalyst according to the present invention is a method for producing the above exhaust gas purifying catalyst, wherein the secondary particle aggregate of the first compound is atomized and the noble metal comes into contact. Including a step of setting the secondary particle diameter of the first compound to 2 μm or less and a step of forming a second compound around the first compound in contact with the atomized noble metal. You can also

  The exhaust gas purification catalyst according to the present invention has excellent exhaust gas purification performance when used for an engine that operates on the lean side of the stoichiometric ratio, such as a direct injection engine or a diesel engine. have.

  According to the method for producing an exhaust gas purification catalyst of the present invention, the exhaust gas purification catalyst of the present invention having the above effects can be easily produced.

  Hereinafter, embodiments of an exhaust gas purifying catalyst of the present invention will be described with reference to the drawings.

  FIG. 1 is a schematic diagram of an exhaust gas purifying catalyst according to an embodiment of the present invention. The exhaust gas purifying catalyst 1 shown in FIG. 1 has a noble metal particle 2 having catalytic activity, a first compound 3 that contacts the noble metal particle 2 and suppresses the movement of the noble metal particle 2, and the noble metal particle 2. The second compound 4 includes the first compound 3 and suppresses the movement of the noble metal particles 2 and suppresses the aggregation of the first compound 3 due to the contact between the first compounds 3. The first compound 3 carries noble metal particles 2. In addition, a plurality of aggregates of the first compounds 3 carrying the noble metal particles 2 are included in the compartments separated by the second compounds 4.

  In the exhaust gas purifying catalyst 1 having such a structure, the noble metal particles 2 and the first compound 3 are brought into contact with each other and supported, whereby the first compound 3 acts as an anchor agent for chemical bonding. Chemically inhibits the movement of particles. Moreover, the movement of the noble metal particle 2 is physically suppressed by covering the noble metal particle 2 with the first compound 3 with the second compound 4 and enclosing it. Further, by containing the noble metal particles 2 and the first compound 3 in the section separated by the second compound 4, the first compound 3 crosses the section separated by the second compound 4. Suppresses contact and aggregation. For these reasons, the exhaust gas purifying catalyst 1 can prevent a decrease in catalytic activity due to aggregation of the noble metal particles 2 without increasing the manufacturing cost and environmental load, and the noble metal particles due to the first compound 3 can be prevented. 2 activity improvement effect can be maintained.

  The present invention is characterized in that the first compound contains Ti as a main component. In a conventional exhaust gas purifying catalyst in which the first compound is made of an oxide containing Ce as a main component, when applied to a gasoline direct-injection engine and a diesel engine operated on the lean side of stoichiometry, the atmosphere Since a large amount of oxygen is present in the inside, there is a possibility that a nearby noble metal may be adsorbed and poisoned by excessive oxygen adsorption at a low temperature, and noble metal oxidation may be caused by excessive oxygen release at a high temperature.

  On the other hand, in the present invention, Ti having an anchoring action, lower oxygen absorption / release capacity than Ce and having a basic surface like Ce is used as the first compound. Thus, a catalyst that is required to be purified by oxidizing the exhaust gas in an atmosphere from stoichiometric to lean while maintaining the durability improvement of the noble metal by having the structure shown in FIG. This significantly improves the oxidation performance. In particular, since the exhaust gas purifying catalyst of the present invention can effectively oxidize HC in exhaust gas components, especially methane, which is difficult to oxidize and purify, the performance improvement cost is large.

In the exhaust gas purifying catalyst of the present invention, the reason why the oxidation performance of the above-described catalyst is remarkably improved is not necessarily clear. However, the first compound is a compound mainly composed of Ti. This is thought to be due to the suppression of For example, when the precious metal is Pt, it is known that the state changes to the state of metal Pt, PtO, PtO ₂ depending on the degree of oxidation. Among these states, the metal Pt has the highest oxidation performance of exhaust gas. The oxidation performance decreases in the order of metal Pt → PtO → PtO ₂ . The inventors have clarified that the oxidation state of such a noble metal also changes in the reaction atmosphere, but also changes depending on the physical properties of the substrate supporting the noble metal particles, that is, the physical properties of the first compound in the present invention. . In particular, in the case where the first compound supported is a compound containing Ti as the main component, Pt tends to take an electronic state close to that of metal Pt, as compared with the case where it is a compound containing Ce as the main component, and oxidation activity. Will improve. This change can be observed by XPS. From the above, in the present invention, the oxidation activity of the catalyst can be improved by using Ti as the first compound.

  The noble metal has a catalytic action and is at least one element selected from [Pt, Pd and Rh] suitable for use in an exhaust gas purifying catalyst.

The second compound is selected from [Al and Si] as a material having heat resistance and capable of forming pores that allow the exhaust gas to reach the noble metal particles 2 included in the second compound 4. A compound having one or more as a main component. Specifically, Al ₂ O ₃ , SiO ₂ , Al—Si composite oxide and the like can be applied. The second compound may be a mixture of Al ₂ O ₃ and SiO ₂ .

The exhaust gas purifying catalyst unit of the present invention, that is, the noble metal is supported on the first compound, the first compound on which the noble metal is supported is encapsulated in the second compound, and the noble metal is supported on the first compound. The unit having a structure in which the first compounds are separated from each other by the second compound preferably includes a unit in which the amount of the noble metal in the unit is 8 × 10 ⁻²⁰ mol or less.

  FIG. 2 is a schematic view showing an example of a unit of the exhaust gas purifying catalyst of the present invention. The exhaust gas purifying catalyst 1 shown in FIG. 1 includes noble metal particles 2, a first compound 3 supporting the noble metal particles 2, and a second compound 4 containing the noble metal particles 2 and the first compound 3. This point is the same as the exhaust gas purifying catalyst 1 shown in FIG. The noble metal particles 2 and the first compound 3 are contained in various modes in the compartments separated by the second compound 4.

  In FIG. 2, among the units having a structure separated by the second compound 4, the unit U <b> 1 includes a single first compound 3 carrying a single noble metal particle 2. Further, in the unit U2, a plurality of first compounds 3 carrying a plurality of noble metal particles 2 are contained as aggregates (secondary particles). In the units U3 to U6, a single first compound 3 carrying a plurality of noble metal particles 2 is contained in various particle sizes.

  Each of the units U1 to U6 of the exhaust gas purifying catalyst 1 shown in FIG. 2 is the same as the exhaust gas purifying catalyst 1 shown in FIG. 1 beyond the section separated by the second compound 4. It is suppressed that 1 compound 3 contacts and aggregates. Therefore, it has the same effect as the exhaust gas purifying catalyst 1 shown in FIG.

In the unit having a structure separated by the second compound 4, it is preferable to contain precious metal particles in an amount of 8 × 10 ⁻²⁰ mol or less in total. As shown in FIG. 2, the noble metal particles 2 and the first compound 3 included in the compartments separated by the second compound 4 have various modes. When the exhaust gas purifying catalyst is put to practical use, a plurality of noble metal particles 2 may move in these compartments due to the high temperature of the atmosphere and agglomerate with each other. In this case, the precious metal particles 2 do not move to the second compound 4 due to the effect of the first compound 3 as the anchor agent in any of the units U1 to U6, and only one or a plurality of the precious metal particles 2 are present in the unit. Aggregates into noble metal particles. An example of before and after aggregation of the noble metal particles 2 in one unit is schematically shown in FIGS. 3 (a) and 3 (b).

  Here, even if the noble metal particles are aggregated in one unit, if the particle size of the aggregated noble metal particles is 10 nm or less, sufficient catalytic activity is exhibited, and deterioration of the catalytic activity due to aggregation is suppressed. Can do. FIG. 4 is a graph showing the relationship between the noble metal particle diameter and the noble metal surface area for platinum or palladium as a noble metal having catalytic activity. In the figure, since the curves are almost the same when the noble metal is platinum and palladium, they are shown as one curve. As is clear from the figure, if the particle diameter of the noble metal is 10 [nm] or less, the particle surface area is large and sufficient activity can be obtained, so that deterioration of the catalyst activity due to aggregation can be suppressed.

FIG. 5 is a graph showing the relationship between the noble metal particle diameter and the number of noble metal atoms for platinum or palladium as a noble metal having catalytic activity. In the figure, since the curves are almost the same when the noble metal is platinum and palladium, they are shown as one curve. As is clear from the figure, the number of atoms when the particle diameter of the noble metal is 10 [nm] is about 48,000, and when this value is converted into the number of moles, the amount is about 8 × 10 ⁻²⁰ moles or less. .

From these viewpoints, in any of the units U1 to U6, by limiting the amount of noble metal in the unit and making it an amount of 8 × 10 ⁻²⁰ mol or less, it aggregates into one in the unit. Also, it is possible to suppress the deterioration of the catalyst activity.

As a means for reducing the amount of the noble metal contained in the unit to 8 × 10 ⁻²⁰ mol or less, the supporting concentration of the noble metal particles 2 of the first compound 3 is lowered, or the first compound 3 supporting the noble metal particles 2 is used. There are two means of reducing the particle size of the. In the present invention, although not limited to these means, when actual catalyst production is considered, the former method of lowering the supported concentration can be used for exhaust gas purification in order to maintain the performance of a predetermined exhaust gas purification catalyst. Since the volume of the honeycomb carrier coated with the catalyst has to be increased, and therefore, it is necessary to coat the honeycomb carrier with a coating amount that is usually an order of magnitude larger than that of the catalyst, it is not practical.

Regarding the particle diameter of the first compound 3, the median particle diameter is preferably 2 [μm] or less . In the present invention, the particle size of the first compound 3 dispersed independently refers to the secondary particle size. The first compound 3 has a function as an anchor agent that contacts the noble metal particles 2 and suppresses the movement of the noble metal particles 2. The anchor effect of this anchor agent is affected by the size of the first compound 3 itself. Like the conventional exhaust gas purifying catalyst, the above-mentioned sufficient precious metal aggregation suppressing effect is exhibited even when a noble metal is impregnated and supported on a powdery first compound such as Ti oxide and dispersed in alumina. It is difficult. For example, when the particles of the first compound 3 are obtained by a pulverization method using a conventional ball mill or the like, only a particle size of 2 to 3 [μm] is obtained at the minimum. An exhaust gas purifying catalyst using three particles of the first compound having a particle size of 2 to 3 [μm] at the minimum, based on the actual upper limit of the coating amount on the cordierite honeycomb carrier and the amount of precious metal used. The exhaust gas purifying catalyst in which the noble metal particles 2 are supported on the first compound 3 particles in a predetermined amount, the noble metal particles 2 aggregate to several tens [nm] when used for a long time at a high temperature. Activity will deteriorate. Therefore, when applied to an actual catalyst, it is preferable that the first compound 3 contained in the compartment separated by the second compound 4 has a median diameter of 2 [μm] or less. The first compound having an average particle size of 2 [μm] or less will be described in detail in the description of the production method described later. The first compound carrying a noble metal may be made into a fine colloid. It can be obtained by appropriately applying a pulverization method using an apparatus capable of pulverizing to 2 [μm] or less.

  The lower limit of the average particle size of the first compound 3 is determined as the particle size of the first compound 3 that can be produced by an industrial manufacturing process, and is not particularly limited.

More specifically, the first compound according to the present invention containing Ti as a main component is preferably an oxide containing Ti. The oxide containing Ti may be an oxide in which the metal element is only Ti, that is, a Ti oxide such as TiO ₂ , but is a composite oxide of Ti and a third compound. More preferably, the compound 3 is a compound of at least one element selected from [Ce, Zr, Ba, Mg, W, Nd and Y]. In addition to Ti, it is possible to add one or more third compounds to the first compound. [Ce, Zr, Ba, Mg, W, Nd and Y] are all effective components added to the first compound of the present invention as subcomponents. By adding at least one element selected from [Ce, Zr, Ba, Mg, W, Nd and Y] or a compound thereof to the first compound, it is possible to promote the adsorption of acidic substances by increasing the surface base. The effect of improving the heat resistance and the like by stabilizing the crystal structure of the first compound can be obtained by adding the subcomponent element. Examples of the third compound include oxides of subcomponent elements such as CeO ₂ , ZrO ₂ , BaO, MgO, WO ₃ , Nd ₂ O ₃ , and Y ₂ O ₃ . Further, the content ratio of the third compound in the first compound is not particularly limited, but in the present invention, the first compound is mainly composed of Ti, and therefore the third compound is less than 50 mol%. It is.

  Further, the first compound is not limited to the composite oxide of the Ti oxide and the third compound described above, but may be a mixture of the Ti oxide and the third compound.

The second compound contains as a main component one or more selected from [Al and Si], and may further include one or more selected from [La, Zr, Ce, Y, and Nd]. [La, Zr, Ce, Y and Nd] are all effective components added to the second compound of the present invention as subcomponents. By adding at least one element selected from [La, Zr, Ce, Y and Nd] or a compound thereof to the second compound, it is possible to promote adsorption of acidic substances by increasing the surface base, Effects such as improvement of heat resistance can be obtained by stabilizing the crystal structure of the second compound by adding the element. By adding at least one element selected from [La, Zr, Ce, Y and Nd] to the second compound, and the second compound is a composite oxide with one or more selected from [Al and Si] In this case, specific examples of oxides of [La, Zr, Ce, Y, and Nd] as constituent elements of the composite oxide include La ₂ O ₃ , ZrO ₂ , CeO ₂ , Y ₂ O ₃ , Nd ₂ O ₃ , etc. Further, the content ratio of at least one element selected from [La, Zr, Ce, Y, and Nd] in the second compound or the compound thereof is not particularly limited, but in the present invention, the second compound is [Al And Si]], the main component being one or more selected from Si].

  Next, the manufacturing method of the exhaust gas purifying catalyst of the present invention will be described. First, a step of supporting a noble metal on the first compound is performed. The step of supporting the noble metal on the first compound can be, for example, a step of making the first compound in contact with the noble metal into a colloidal form having a primary particle diameter of 100 nm or less. As another example, the secondary particle aggregate of the first compound can be atomized so that the secondary particle diameter of the first compound in contact with the noble metal is 2 μm or less.

  The former step of making the first compound in contact with the noble metal into a colloidal form having a primary particle diameter of 100 nm or less will be described below. This step can be a step of preparing a colloid of the first compound commercially available or separately prepared, and bringing the noble metal into contact with the colloid of the first compound. Specifically, a noble metal salt is added to and dispersed in the colloid of the first compound, and then the noble metal is brought into contact by reducing and precipitating the noble metal on the surface of the first compound using a reducing agent such as ethanol. Alternatively, the noble metal is brought into contact by adding a noble metal colloid to the colloid of the first compound.

  In the explanatory diagram of this process shown in FIG. 6, the place where the noble metal particles 2 are in contact with the first compound 3 by this process is schematically shown on the left side of the arrow. In this step, the colloid of the first compound can be wrapped with the protective material for dispersion before the contact with the noble metal particles 2 or can be wrapped with the protective material for dispersion after the contact with the noble metal particles. . The right side of the arrow in FIG. 6 schematically shows that the protective material 7 for dispersion is formed so as to wrap the first compound 3 in contact with the noble metal particles 2. The dispersion protective material 7 is, for example, a polymer compound (polymer), nitric acid, acetic acid, or the like, and can more effectively suppress the aggregation of the first compound 3 in contact with the noble metal particles 2. In the method for producing an exhaust gas purifying catalyst, it may be used as necessary and is not essential.

  By the above process, the first compound in contact with the noble metal is uniformly dispersed in the colloidal solution, so that the first compounds in contact with the noble metal particles are prevented from aggregating in the solution. Thereby, the secondary particle diameter of the first compound of the exhaust gas purifying catalyst manufactured through the post-process can be easily reduced to 2 μm or less in average particle diameter. In order to set the secondary particle size of the first compound of the exhaust gas purifying catalyst to an average particle size of 2 μm or less, the primary particle size of the colloid is preferably 100 nm or less.

  Next, among the steps mentioned above as the step of supporting the noble metal on the first compound, the latter, the second particle aggregate of the first compound, is atomized, and 2 of the first compound in contact with the noble metal is contacted. A process for setting the next particle size to 2 μm or less will be described. This step is a combination of preparing a first compound having a particle size on the order of microns, crushing the first compound, and supporting a noble metal on the first compound. The order of crushing the first compound and supporting the noble metal on the first compound is not particularly limited. For example, after precious metal particles are supported on the first compound, they can be crushed. In addition, noble metal particles can be supported during pulverization of the first compound. Furthermore, after pulverizing the first compound, the noble metal particles can be supported.

  As a method for supporting the noble metal particles on the first compound, an impregnation method, a spray method, a kneading method, or the like can be appropriately used. In addition, the precursor salt of the noble metal or the noble metal colloid and the precursor salt of the first compound are mixed in an aqueous solution, and then the precursor salt of the first compound is insolubilized and the solvent is removed. A method in which a part of the noble metal is included in the first compound by firing later may be used.

  The first compound is crushed by using a pulverizer such as a vibrating ball mill, a planetary ball mill, a bead mill, a jet mill, etc., and using a secondary pulverization method such as wet pulverization, dry pulverization, or ultrasonic pulverization. A pulverization method capable of reducing the particle diameter to 2 μm or less can be appropriately used. By grinding the first compound, the secondary particle size of the first compound of the exhaust gas purifying catalyst finally obtained by the production method of the present invention can be reduced to 2 μm or less.

  After pulverization, it can be colloided by mixing with a protective material for dispersion made of a polymer such as polyethyleneimide and polymethacrylic acid. This colloidalization can stabilize the fine dispersion state of the first compound carrying the noble metal. This colloidalization method can also be used as appropriate, for example, by mixing with a polymer protective material. In addition, it is possible to maintain the dispersion state up to the next step by ultrasonic dispersion or the like.

  By pulverizing the first compound, the first compound on which the noble metal is supported becomes fine particles of about several tens to several hundreds of nanometers, and is included in the second compound in the subsequent steps. It is included as a fine unit. Therefore, there is little aggregation of the first compounds after durability, and a highly active catalyst can be obtained.

  Next, in the method for producing an exhaust gas purifying catalyst of the present invention, after the step of supporting the noble metal on the first compound as described above, the periphery of the first compound in contact with the atomized noble metal is provided. And a step of forming a second compound.

  An example of this process will be described with reference to the schematic explanatory view of FIG. The raw material of the second compound is added to the fine first compound 3 on which the noble metal particles 2 are supported as shown on the left side of the figure. As a result, as shown in the center of FIG. 7, the precursor 8 of the second compound is formed around the fine first compound 3 on which the noble metal particles 2 are supported. The forming method may be an impregnation method or an inclusion method. Next, as shown on the right side of FIG. 7, the solid content of the colloidal solution in which the precursor 8 of the second compound is formed is separated, dried by distilling off the water, and then calcined. The precursor 8 of the second compound is changed to the second compound 4. In this way, the exhaust gas purifying catalyst of the present invention is obtained. Distillation of water includes distillation of water by heating in a bat or the like, electromagnetic heating such as microwaves, vacuum drying using an evaporator, spray heating using spray drying, freeze drying using freeze drying, etc. It can be used as appropriate.

  The exhaust gas purifying catalyst of the present invention is applied and formed on a refractory honeycomb carrier or the like and used for exhaust gas purification of an actual engine.

  Hereinafter, the present invention will be specifically described based on examples.

[Method for producing catalyst powder]
Catalysts of Examples 1 to 6 and Comparative Examples 1 and 2 shown in Table 1 were prepared. The production methods of these catalysts are as described below.

[Example 1]
Commercially available acicular rutile TiO ₂ (primary particle size 3 [μm]) as a raw material for the first compound was pulverized in pure water with a wet pulverizer and measured with a laser scattering particle size distribution meter. The diameter was 200 [nm]. A dinitrodiamine Pt aqueous solution (Pt concentration of 8.47 [wt%]) was dispersed in the pulverized slurry containing the first compound, and stirred for about 2 hours to obtain a slurry containing the first compound in contact with Pt. . On the other hand, boehmite slurry in which boehmite, cerium nitrate, zirconium nitrate oxide and pure water were mixed was obtained. This slurry was mixed with the slurry containing the first compound in contact with the Pt, and stirred with a high-speed stirrer.

  The water in the slurry after stirring was distilled off to 5% or less, dried at 150 [° C.] for 12 hours, and then fired at 400 [° C.] for 1 hour in an air stream.

As a result, a catalyst in which Pt particles of noble metal were supported on TiO ₂ of the first compound and further covered with Ce-Zr-AlOx of the second compound was obtained. In addition, the mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values shown in Table 1.

[Example 2]
A TiO ₂ —ZrO ₂ composite compound prepared by a coprecipitation method as a raw material for the first compound is pulverized in pure water by a wet pulverizer, and the median diameter measured by a laser scattering particle size distribution analyzer is 300 [ nm]. A dinitrodiamine Pt aqueous solution (Pt concentration of 8.47 [wt%]) is dispersed in the slurry containing the first compound after pulverization, and after stirring for about 2 hours, a PEI (polyethyleneimine) solution is further added as a protective material for dispersion. The mixture was mixed with 20 wt%, and further colloided by stirring for 2 hours. Meanwhile, boehmite slurry in which boehmite, lanthanum nitrate oxide and pure water were mixed was obtained. This slurry was mixed with the slurry containing the first compound in contact with the Pt, and stirred with a high-speed stirrer.

  The water in the slurry after stirring was distilled off to 5% or less, dried at 150 [° C.] for 12 hours, and then fired at 400 [° C.] for 1 hour in an air stream.

As a result, a catalyst in which Pt particles of noble metal were supported on the TiO ₂ —ZrO ₂ composite compound of the first compound and covered with La—AlOx of the second compound was obtained. In addition, the mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values shown in Table 1.

Example 3
Disperse a dinitrodiamine Pt aqueous solution (Pt concentration 8.47 [wt%]) in commercially available titania sol (primary particle size 30 [nm]) and barium nitrate as raw materials for the first compound, stir for about 2 hours and stir Pt. A suspension containing the first compound contacted was obtained. On the other hand, aluminum isopropoxide was mixed in hexylene glycol to prepare a solution dissolved in an oil bath at 120 [° C.]. In this hexylene glycol solution of aluminum isopropoxide, the suspension of the previous mixture was slowly dropped in an oil bath of 80 [° C.] to form aluminum hydroxide around Pt, titania sol and barium nitrate. .

  Thereafter, the oil bath temperature was gradually raised while stirring under reduced pressure, and the solvent was distilled off. The obtained powder was dried at 80 [° C.] for 6 hours and further at 150 [° C.] for 12 hours, and then calcined at 400 [° C.] for 1 hour in an air stream.

As a result, a TiO ₂ —BaO composite oxide of the first compound was present around the noble metal Pt particles, and a catalyst covered with alumina of the second compound was obtained. The mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values shown in Table 1.

Example 4
A TiO ₂ -CeO ₂ composite compound prepared by a coprecipitation method as a raw material for the first compound was pulverized in pure water with a wet pulverizer, and the median diameter measured with a laser scattering particle size distribution meter was 350 nm. . A dinitrodiamine Pt aqueous solution (Pt concentration of 8.47 [wt%]) was dispersed in the slurry containing the first compound after pulverization, and the mixture was stirred for about 2 hours. Meanwhile, boehmite slurry in which boehmite, yttrium nitrate and pure water were mixed was obtained. This slurry was mixed with the slurry containing the first compound in contact with the Pt, and stirred with a high-speed stirrer.

  The water in the slurry after stirring was distilled off to 5% or less, dried at 150 [° C.] for 12 hours, and then fired at 400 [° C.] for 1 hour in an air stream.

As a result, a catalyst in which Pt particles of noble metal were supported on the TiO ₂ -CeO ₂ composite compound of the first compound and covered with Y-AlOx of the _second compound was obtained. In addition, the mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values shown in Table 1.

Example 5
Commercially available block-like rutile TiO ₂ (primary particle size 2 [μm]) and magnesium nitrate as raw materials for the first compound are pulverized in pure water using a wet pulverizer and measured with a laser scattering particle size distribution analyzer. The median diameter was 250 [nm]. An aqueous Pd nitrate solution (Pd concentration 20.71 [wt%]) was dispersed in the slurry containing the first compound after pulverization, and stirred for about 2 hours to obtain a slurry containing the first compound in contact with Pd. On the other hand, boehmite slurry in which boehmite, neodymium nitrate and pure water were mixed was obtained. This slurry was mixed with the slurry containing the first compound in contact with Pd, and stirred with a high-speed stirrer.

  The water in the slurry after stirring was distilled off to 5% or less, dried at 150 [° C.] for 12 hours, and then fired at 400 [° C.] for 1 hour in an air stream.

As a result, a catalyst in which Pd particles of noble metal were supported on the TiO ₂ —MgO composite compound of the first compound and covered with Nd—AlOx of the second compound was obtained. In addition, the mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values shown in Table 1.

Example 6
As a raw material for the first compound, a commercially available titania sol (primary particle size 30 [nm]) and neodymium nitrate were dispersed in an aqueous Rh nitrate solution (Rh concentration 8.36 [wt%]), and stirred for about 2 hours to contact Rh. A suspension containing the first compound was obtained. On the other hand, tetraethoxysilane was mixed in hexylene glycol to prepare a solution dissolved in an oil bath at 120 [° C.]. In this hexylene glycol solution such as tetraethoxysilane, the suspension of the above mixture is slowly dropped in an oil bath at 80 [° C] to form a SiO ₂ precursor around Rh, titania sol, and neodymium nitrate. did.

  Thereafter, the oil bath temperature was gradually raised while stirring under reduced pressure, and the solvent was distilled off. The obtained powder was dried at 80 [° C.] for 6 hours and further at 150 [° C.] for 12 hours, and then calcined at 400 [° C.] for 1 hour in an air stream.

As a result, a TiO ₂ —Nd ₂ O ₃ composite oxide of the first compound was present around the noble metal Rh particles, and a catalyst covered with SiO ₂ of the second compound was obtained. The mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values shown in Table 1.

[Comparative Example 1]
Comparative Example 1 is an example in which the first compound supporting a noble metal is CeO ₂ —ZrO ₂ .

A commercially available CeO ₂ —ZrO ₂ composite compound (primary particle size 30 [nm]) as a raw material for the first compound was pulverized in pure water with a wet pulverizer and measured with a laser scattering particle size distribution analyzer. The median diameter was 200 [nm]. A dinitrodiamine Pt aqueous solution (Pt concentration of 8.47 [wt%]) was dispersed in the slurry containing the first compound after pulverization, and stirred for about 2 hours to obtain a slurry containing the first compound in contact with Pt. . On the other hand, boehmite slurry in which boehmite, cerium nitrate, zirconium nitrate oxide and pure water were mixed was obtained. This slurry was mixed with the slurry containing the first compound in contact with the Pt, and stirred with a high-speed stirrer.

  The water in the slurry after stirring was distilled off to 5% or less, dried at 150 [° C.] for 12 hours, and then fired at 400 [° C.] for 1 hour in an air stream.

As a result, a catalyst in which Pt particles of noble metal were supported on the CeO ₂ —ZrO ₂ composite compound of the first compound and further covered with Ce—Zr—AlOx of the second compound was obtained. The mol% of each component of the mixture in each of the first compound and the second compound was adjusted to the values in Table 1.

[Comparative Example 2]
Comparative Example 2 is an example of a conventional general catalyst that does not have the second compound.

Commercially available Al ₂ O ₃ (primary particle size 3 [μm]) is dispersed in dinitrodiamine Pt aqueous solution (Pt concentration 8.47 [wt%]) and pure water, stirred for about 2 hours, and then the water content is reduced to below 5% After distilling off and drying at 150 [° C.] for 12 hours, firing was performed at 400 [° C.] for 1 hour in an air stream.

Thus, a catalyst in which noble metal Pt particles were supported on Al ₂ O ₃ as a carrier was obtained. In Comparative Example 2, the mol% of alumina in the carrier was 100% as shown in Table 1.

[Durability conditions]
The catalyst powders of Examples 1 to 6 and Comparative Examples 1 and 2 produced as described above were calcined at 700 [° C.] and 5 [hr] in an air stream.

[Catalyst performance evaluation]
About each catalyst after the above-mentioned endurance treatment, simulated exhaust gas was circulated with the reaction gas composition and gas flow rate conditions shown in Table 2 using a catalytic reactor TPD-1-AT manufactured by Bell Japan Co., Ltd. ], The CH ₄ conversion rate (ηCH ₄ ) [%] at 400 [° C.] of each of the exhaust gas purifying catalysts of Examples 1 to 6 and Comparative Examples 1 and 2 is calculated from the CH ₄ concentration on the inlet side and the outlet side of Calculated. The sample amount was 0.1 g, and the detector was Q-MASS. The CH ₄ conversion values are also shown in Table 1.

As can be seen from Table 1, the catalyst powders of Examples 1 to 6 are much more excellent in CH ₄ conversion after the durability treatment than the catalyst powders of Comparative Examples 1 and 2. This is presumably because the conversion ratio with respect to CH _{4 is} particularly improved because the first compound is an oxide containing Ti.

  As mentioned above, although the embodiment to which the invention made by the present inventors was applied has been described, the present invention is not limited by the description and the drawings that form part of the disclosure of the present invention according to this embodiment. That is, it should be added that other embodiments, examples, operation techniques, and the like made by those skilled in the art based on the above embodiments are all included in the scope of the present invention.

It is a schematic diagram which shows the structure of the exhaust gas purification catalyst used as embodiment of this invention. It is a schematic diagram which shows the structure of the exhaust gas purification catalyst which becomes another embodiment of this invention. It is a schematic diagram which shows an example before and behind aggregation of the noble metal particle 2 in one unit. It is a graph which shows the relationship between a noble metal particle diameter and a noble metal surface area. It is a graph which shows the relationship between a noble metal particle diameter and the number of atoms of a noble metal. It is explanatory drawing of an example of the process in the manufacturing method of this invention. It is explanatory drawing of an example of the process in the manufacturing method of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Exhaust gas purification catalyst 2 Noble metal particle 3 1st compound 4 2nd compound

Claims (6)

A noble metal, a first compound, made from a second compound, the noble metal is supported on the first compound, the first compound in which the noble metal is supported is encapsulated in the second compounds, the noble metal comprises units of the supported first compounds to each other separated by the second compound structure, and,
The noble metal is made of Pt ,
Wherein said first compound is mainly composed of Ti, and _consists TiO _2, TiO ₂ -ZrO ₂ complex compound or _TiO 2 -CeO ₂ composite compound,
The exhaust gas purifying catalyst, wherein the second compound contains one or more selected from [Al and Si] as a main component. The amount of the noble metal in the unit, an exhaust gas purifying catalyst according to claim 1, wherein the der Turkey 8 × 10 ^-20 mol or less.   The exhaust gas purification catalyst according to claim 1 or 2, wherein the median particle size of the first compound dispersed independently is 2 µm or less. The exhaust gas purification catalyst according to any one of claims 1 to 3 , wherein the second compound further includes one or more selected from [La, Zr, Ce, Y, and Nd]. . A method for producing the exhaust gas purifying catalyst according to any one of claims 1 to 4 ,
Making the first compound in contact with the noble metal colloidal with a primary particle size of 100 nm or less;
And a step of forming a second compound around the first compound in contact with the colloidal noble metal. A method for producing an exhaust gas purifying catalyst. A method for producing the exhaust gas purifying catalyst according to any one of claims 1 to 4 ,
The step of atomizing the secondary particle aggregate of the first compound to make the secondary particle diameter of the first compound in contact with the noble metal 2 μm or less;
And a step of forming a second compound around the first compound in contact with the atomized noble metal. A method for producing an exhaust gas purifying catalyst, comprising:

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